CN112429763A - Method for large-batch synthesis of cuprous oxide nano-cubic blocks based on continuous kettle type device - Google Patents
Method for large-batch synthesis of cuprous oxide nano-cubic blocks based on continuous kettle type device Download PDFInfo
- Publication number
- CN112429763A CN112429763A CN202011452830.XA CN202011452830A CN112429763A CN 112429763 A CN112429763 A CN 112429763A CN 202011452830 A CN202011452830 A CN 202011452830A CN 112429763 A CN112429763 A CN 112429763A
- Authority
- CN
- China
- Prior art keywords
- reaction
- kettle
- continuous
- raw material
- mixer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G3/00—Compounds of copper
- C01G3/02—Oxides; Hydroxides
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/30—Particle morphology extending in three dimensions
- C01P2004/38—Particle morphology extending in three dimensions cube-like
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
The invention discloses a method for synthesizing cuprous oxide nano cubic blocks in large batch based on a continuous kettle type device. The method for synthesizing the cuprous oxide nano cube comprises the following steps: 1) preparing a reaction raw material A which is a mixed solution of copper sulfate, sodium citrate and sodium hydroxide, 2) preparing a reaction raw material B which is an ascorbic acid solution, 3) mixing the raw materials through a micro mixer, then feeding the mixed raw materials into a serial continuous reaction kettle for mixing and reaction, collecting reaction products through a collection kettle, and 4) diluting, centrifuging, separating and washing the collected product solution to obtain cuprous oxide nano cubic blocks. The invention realizes the continuous synthesis of cuprous oxide nano cubic blocks, has good stability and high yield, and is suitable for mass production.
Description
Technical Field
The invention belongs to the technical field of chemical industry and nano materials, and particularly relates to a method for synthesizing cuprous oxide nano cubic blocks in large batch based on a continuous kettle type device.
Background
Cuprous oxide is a P-type semiconductor material, and many researches on cuprous oxide have been carried out, such as gas sensing, photodegradation, photolysis, and lithium ion batteries. In industrial production, the copper oxide can be used as coating, bactericide, catalyst, flame retardant material, electrode material, information storage material and the like, and the continuous production of the cuprous oxide in industry is of practical and economic significance.
Of the many forms that cuprous oxide has, the nano-cubes represent the most important crystal structure of cuprous oxide, since other concentrated crystal forms (e.g., nanocages, octahedrons, or more complex structures) can be produced by transforming the form of cuprous oxide. However, in recent reports, the synthesis of cubic blocks of cuprous oxide has not been able to achieve good results, such as the generation of some distorted cubic or irregularly shaped by-product particles. In the literature, a large amount of surfactants are used for controlling the morphology, the single reaction time is long, the temperature is often high, the obtained cuprous oxide cubic block is often seriously agglomerated, and the particle size distribution is not good enough. These methods all adopt a batch production method, cannot perform continuous production, and have difficulty in controlling the consistency between batches.
Disclosure of Invention
The invention aims to develop a continuous reaction system and a method for synthesizing a novel nano material, and realizes the efficient, rapid and continuous preparation of the cuprous oxide nano cube.
In order to solve the problems of difficult amplification, low stability, low production efficiency and the like in the existing batch synthesis method, the invention provides the following technical scheme:
the invention provides a method for synthesizing cuprous oxide nano cubic blocks in large batch based on a continuous kettle type device, which comprises the following steps:
1) preparing a reaction raw material A which is a mixed solution of copper sulfate, sodium citrate and sodium hydroxide;
2) preparing a reaction raw material B which is an ascorbic acid solution;
3) mixing the raw material A and the raw material B through a micro mixer to form reaction liquid, allowing the reaction liquid to enter a series-connected continuous reaction kettle for reaction, and collecting a reaction product through a collection kettle;
4) diluting, centrifuging, separating and washing the collected product solution to obtain the cuprous oxide nano cubic material.
Further, the method is characterized in that in the step 1), the content of copper sulfate in the raw material A is 1.5mmol/100mL, the content of sodium citrate is 0.51mmol/100mL, and the content of sodium hydroxide is 25mmol/100 mL; in the step 2), the content of ascorbic acid in the raw material B is 3mmol/100mL, and the feeding volume ratio of the raw material A to the raw material B is 2: 1.
Further, the solvent of the solution of the raw materials A and B is deionized water.
Furthermore, the continuous reaction kettles connected in series are jacketed reaction kettles, the temperature is controlled to be 20-25 ℃ and 30-35 ℃ respectively, and the residence time in the reaction kettles is controlled to be 1-5min and 35-40min respectively.
Further, the time sequence of the step 1) and the step 2) is not sequential, and can also be carried out simultaneously.
Further, the continuous tank apparatus comprises: the device comprises a micro mixer, a continuous reaction kettle and a collection kettle, wherein the continuous reaction kettle and the collection kettle are connected in series, the micro mixer is connected with the continuous reaction kettle, and the continuous reaction kettle is connected with the collection kettle.
Furthermore, the continuous reaction kettles connected in series are jacketed reaction kettles, jackets for heat exchange are arranged outside the inner walls of the continuous reaction kettles, a stirring device is arranged on the continuous reaction kettles, and the collecting kettles are provided with stirrers.
Further, the micro mixer is a caterpillar type micro-channel mixer, a micro-sieve hole dispersing mixer or a vortex mixer; the caterpillar type micro-channel mixer at least comprises a branch intersection channel with the hydraulic diameter of 0.2mm-0.5mm, the micro-sieve pore dispersing mixer at least comprises 1 micro-sieve pore with the diameter of 0.1mm-0.3mm and a corresponding mixing channel, and the eddy type mixer at least comprises an eddy generation area with the diameter of 1mm and a corresponding mixing channel.
The invention solves the problems of difficult amplification, low stability, low production efficiency and the like in the existing batch synthesis method, realizes the continuous synthesis of the up-conversion nano material, and has the following advantages:
1. the new synthesis method can be carried out at near room temperature, and is energy-saving and environment-friendly;
2. the reaction device is operated continuously, the labor cost is low, the production efficiency is high, and the scale-up experiment is easy; a
3. Multi-stage temperature control is favorable for process control, and the safety of the reaction is greatly improved.
Drawings
FIG. 1: the invention relates to a continuous kettle type device for synthesizing cuprous oxide nano cubic blocks.
Detailed Description
The invention will be further elucidated and explained with reference to the embodiments and the drawings.
The invention relates to a continuous kettle type device for synthesizing cuprous oxide nano cubic blocks based on a continuous reaction kettle device, which comprises: 1 micromixer (1), 2 continuous reaction kettles (2, 3) and 1 collection kettle (4), wherein the micromixer (1) is connected with the continuous reaction kettles (2 and 3) which are connected in series, the continuous reaction kettle (3) is connected with the collection kettle (4), and the connection sequence is shown in figure 1.
The process for synthesizing cuprous oxide nano cubic blocks in large batch based on the continuous kettle type device comprises the following steps: mixing a mixed solution (A) containing copper sulfate, sodium citrate and sodium hydroxide with an ascorbic acid solution (B) in a micro mixer (1) to form a reaction solution (C); after flowing out of the micro mixer (1), the reaction liquid (C) flows through the first continuous reaction kettle (2), and the reaction temperature and time are controlled to quickly form precursor reaction liquid (D); the reaction liquid (D) flows out of the first continuous reaction kettle (2), then flows through the second continuous reaction kettle (3), and the reaction temperature and the reaction time are controlled to form reaction liquid (E); and (3) allowing the reaction solution (E) to flow out of the second continuous reaction kettle (3), and collecting the product solution (F) through the collection kettle (4) for subsequent treatment to obtain cuprous oxide nano cubic blocks.
The term "room temperature" as used herein means 15 to 30 ℃.
Examples
A method for synthesizing cuprous oxide nano cubic blocks in large batch based on a continuous kettle type device comprises the following steps:
1) weighing copper sulfate, sodium citrate, sodium hydroxide and ascorbic acid, respectively adding into deionized water at room temperature, and performing ultrasonic treatment until the solution is clear to obtain a mixed solution of copper sulfate, sodium citrate and sodium hydroxide and an ascorbic acid solution.
2) Constructing a continuous reaction kettle device according to the figure 1, conveying the reaction raw materials obtained in the step 1) into a continuous reaction kettle reaction system by using a constant flow pump for reaction, monitoring the temperature of the continuous reaction kettle in real time, and finally collecting the product by using a collection kettle.
3) And sequentially diluting the product solution with deionized water and absolute ethyl alcohol, washing, centrifuging and drying to obtain cuprous oxide nano cubic blocks, and weighing to calculate the yield. The specific experimental conditions and results are as follows:
TABLE 1 tabulation of examples 1-2
Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes and modifications can be made therein by those skilled in the art without departing from the spirit and scope of the invention as defined in the appended claims.
Claims (8)
1. A method for synthesizing cuprous oxide nano cubic blocks in large batch based on a continuous kettle type device is characterized by comprising the following steps:
1) preparing a reaction raw material A which is a mixed solution of copper sulfate, sodium citrate and sodium hydroxide;
2) preparing a reaction raw material B which is an ascorbic acid solution;
3) mixing the raw material A and the raw material B through a micro mixer to form reaction liquid, allowing the reaction liquid to enter a series-connected continuous reaction kettle for reaction, and collecting a reaction product through a collection kettle;
4) diluting, centrifuging, separating and washing the collected product solution to obtain the cuprous oxide nano cubic material.
2. The method as claimed in claim 1), wherein the raw material A in step 1), wherein the content of copper sulfate is 1.5mmol/100mL, the content of sodium citrate is 0.51mmol/100mL, and the content of sodium hydroxide is 25mmol/100 mL; in the step 2), the content of ascorbic acid in the raw material B is 3mmol/100mL, and the feeding volume ratio of the raw material A to the raw material B is 2: 1.
3. The method of claim 1, wherein the solvent of the solution of starting materials a and B is deionized water.
4. The method according to claim 1, wherein the continuous reaction kettles connected in series are jacketed reaction kettles, the temperature is controlled to be 20-25 ℃ and 30-35 ℃ respectively, and the residence time in the reaction kettles is controlled to be 1-5min and 35-40min respectively.
5. The method according to claim 1, wherein the steps 1) and 2) are performed in chronological order, not sequentially, but simultaneously.
6. The method of claim 1, wherein the continuous tank apparatus comprises: the device comprises a micro mixer, a continuous reaction kettle and a collection kettle, wherein the continuous reaction kettle and the collection kettle are connected in series, the micro mixer is connected with the continuous reaction kettle, and the continuous reaction kettle is connected with the collection kettle.
7. The method according to claim 6, wherein the continuous reaction kettles connected in series are jacketed reaction kettles, the jackets for heat exchange are arranged outside the inner walls of the jacketed reaction kettles, the jacketed reaction kettles are provided with stirring devices, and the collecting kettles are provided with stirrers.
8. The method of claim 6, wherein the micromixer is a caterpillar-type microchannel mixer or a micromesh-hole dispersing mixer or a vortex mixer; the caterpillar type micro-channel mixer at least comprises a branch intersection channel with the hydraulic diameter of 0.2mm-0.5mm, the micro-sieve pore dispersing mixer at least comprises 1 micro-sieve pore with the diameter of 0.1mm-0.3mm and a corresponding mixing channel, and the eddy type mixer at least comprises an eddy generation area with the diameter of 1mm and a corresponding mixing channel.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011316369 | 2020-11-20 | ||
| CN2020113163695 | 2020-11-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112429763A true CN112429763A (en) | 2021-03-02 |
Family
ID=74692567
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011452830.XA Pending CN112429763A (en) | 2020-11-20 | 2020-12-11 | Method for large-batch synthesis of cuprous oxide nano-cubic blocks based on continuous kettle type device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112429763A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5409686A (en) * | 1988-08-26 | 1995-04-25 | Norddeutsche Affinerie Aktiengesellschaft | Process for producing yellow copper (I) oxide with narrow particle size range |
| CN101348275A (en) * | 2008-09-11 | 2009-01-21 | 北京航空航天大学 | Preparation of polyhedral cuprous oxide nano particle |
| US20100119828A1 (en) * | 2007-07-25 | 2010-05-13 | Woo-Ram Lee | Spherical assembly particle composition of cuprous oxide and preparation method thereof |
| CN101805011A (en) * | 2010-04-06 | 2010-08-18 | 厦门大学 | Cu2O ultra-fine nano-particles and self-assembly nanospheres as well as preparation method thereof |
| CN107601548A (en) * | 2017-01-13 | 2018-01-19 | 广西民族大学 | A kind of preparation of small size cube cuprous nano material |
| CN108864178A (en) * | 2018-07-19 | 2018-11-23 | 山东默锐科技有限公司 | A kind of synthesis tricresyl phosphate（2- chloropropyl）The micro- reaction method and device of ester |
| CN108941599A (en) * | 2018-07-03 | 2018-12-07 | 珠海市彩龙科技有限公司 | A kind of continuous preparation method of Nanometer Copper |
| CN109810074A (en) * | 2019-02-19 | 2019-05-28 | 蔚林新材料科技股份有限公司 | A kind of reaction unit of continuous synthesis 2-mercaptobenzothiazole |
-
2020
- 2020-12-11 CN CN202011452830.XA patent/CN112429763A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5409686A (en) * | 1988-08-26 | 1995-04-25 | Norddeutsche Affinerie Aktiengesellschaft | Process for producing yellow copper (I) oxide with narrow particle size range |
| US20100119828A1 (en) * | 2007-07-25 | 2010-05-13 | Woo-Ram Lee | Spherical assembly particle composition of cuprous oxide and preparation method thereof |
| CN101348275A (en) * | 2008-09-11 | 2009-01-21 | 北京航空航天大学 | Preparation of polyhedral cuprous oxide nano particle |
| CN101805011A (en) * | 2010-04-06 | 2010-08-18 | 厦门大学 | Cu2O ultra-fine nano-particles and self-assembly nanospheres as well as preparation method thereof |
| CN107601548A (en) * | 2017-01-13 | 2018-01-19 | 广西民族大学 | A kind of preparation of small size cube cuprous nano material |
| CN108941599A (en) * | 2018-07-03 | 2018-12-07 | 珠海市彩龙科技有限公司 | A kind of continuous preparation method of Nanometer Copper |
| CN108864178A (en) * | 2018-07-19 | 2018-11-23 | 山东默锐科技有限公司 | A kind of synthesis tricresyl phosphate（2- chloropropyl）The micro- reaction method and device of ester |
| CN109810074A (en) * | 2019-02-19 | 2019-05-28 | 蔚林新材料科技股份有限公司 | A kind of reaction unit of continuous synthesis 2-mercaptobenzothiazole |
Non-Patent Citations (2)
| Title |
|---|
| 任郑玲: "纳米Cu2O的合成及其光催化性能的研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 * |
| 王栋: "氧化亚铜微粉连续制备的方法研究", 《中国博士学位论文全文数据库工程科技Ⅰ辑》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104650104B (en) | The preparation method of zinc ion-porphyrin nano complex | |
| CN106563811B (en) | A kind of method that sea urchin shape Ag-ZnO nano-particles are continuously prepared using micro passage reaction | |
| WO2011131008A1 (en) | Method for preparing nano-nickel powder with microchannel reactor | |
| CN113929105B (en) | Preparation method of metal organic framework derived nickel silicate | |
| CN107879337A (en) | Prepare the method and its equipment of graphene oxide | |
| CN108079999A (en) | A kind of method of continuous producing carbon nano-tube poly-metal deoxide pore space structure catalyst | |
| CN108299175A (en) | A kind of zinc acetylacetonate preparation process | |
| CN102153129B (en) | Method and device for continuously synthesizing spherical micro-nano cuprous oxide powder | |
| CN110642678A (en) | Method for preparing 2, 5-dichlorophenol by continuously oxidizing p-dichlorobenzene | |
| CN106807317A (en) | A kind of reaction unit for disperseing to mix battery material | |
| CN112210083A (en) | Method for continuously preparing nanometer bimetallic zeolite imidazole ester framework by microreactor | |
| CN108855055A (en) | A kind of preparation method of the high activity hydroxide palladium carbon based on microreactor | |
| CN107999072A (en) | A kind of photo-thermal catalyst, its preparation method and the method for being catalyzed cyclohexane oxidation | |
| CN107673394B (en) | Method for preparing micron-sized triangular conical cuprous bromide by using ultrasonic-assisted microchannel reaction device | |
| CN112429763A (en) | Method for large-batch synthesis of cuprous oxide nano-cubic blocks based on continuous kettle type device | |
| CN104649912B (en) | Method for efficiently separating primary amine and purifying secondary amine by using microreactor | |
| CN114931912B (en) | Microfluidic synthesis device and synthesis method for covalent organic framework material | |
| CN105645481B (en) | A kind of cobaltosic oxide and preparation method thereof | |
| CN216499237U (en) | Equipment for preparing graphene oxide through microfluidics | |
| CN114716358A (en) | Method for continuously synthesizing peroxyacetic acid by using microreactor | |
| CN114713164A (en) | Dibenzothiazole disulfide micro-reaction continuous synthesis system and synthesis method | |
| CN111704157A (en) | Preparation method of microchannel of nano zinc oxide | |
| CN208407002U (en) | A kind of device of continuity method production tetramethyl ammonium carbonate | |
| CN108503519B (en) | Process for preparing 2,3, 5-trimethyl-p-benzoquinone by catalytic oxidation | |
| CN108975409B (en) | Preparation method of small-size high-dispersity trimanganese tetroxide nanoparticles |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210302 |